Module 6 : Heat Transfer in Boiling and Condensation

Lecture 25

At this stage it would be interesting to know the Leidenfrost phenomenon, which was observed by Leidenfrost in 1756. When water droplets fall on a very hot surface they dance and jump on the hot surface and reduces in size and eventually the droplets disappear. The mechanism is related to the film boiling of the water droplets. When water droplet drops on to the very hot surface, a film of vapour forms immediately between the droplet and the hot surface. The vapour film generated provide and up-thrust to the droplet. Therefore, the droplet moves up and when again the droplet comes in the contact of the hot surface, the vapour generated out of the water droplet and the phenomenon continues till it disappears.

The effectiveness of nucleate boiling depends primarily on the ease with which bubbles form and free themselves from the heating surface. The important factor in controlling the rate of bubble detachment is the interfacial tension between the liquid and the heating surface. If this interfacial tension is large the bubbles tends to spread along the surface and blocked the heat transfer area, rather than leaving the surface, to make room for other bubbles. The heat transfer coefficient obtained during the nucleation boiling is sensitive to the nature of the liquid, the type and condition of the heating surface, the composition and purity of the liquid, agitation, temperature and pressure.

Fact: Film boiling is not normally desired in commercial equipment because the heat transfer rate is low for such a large temperature drop.

6.2.1 Nucleation boiling

Rohsenow correlation may be used for calculating pool boiling heat transfer

(6.2)

where,

 

q is the heat flux (W/m2)

 

μl is the liquid viscosity (Pa.s)

 

λ is the enthalpy of liquid vaporisation (J/kg)

 

ρl and ρv are the liquid and vapour density, respectively, (kg/m3)

 

cp1 is the specific heat of liquid (J/kg/°C)

 

σ is the surface tension (N/m)

 

Te is the excess temperature of the boiling surface, Tw - Tsat, (K)

 

Pr1 is the liquid Prandtl number

Csf and n are the constants and depend on the liquid and heating surface combination for boiling operation, for example,

All the properties are to be evaluated at film temperature.